EP3120004B1

EP3120004B1 - Actuation assembly and method of operating an actuator

Info

Publication number: EP3120004B1
Application number: EP15802430.7A
Authority: EP
Inventors: Robert Nyzen; Martin A. Clements
Original assignee: Eaton Corp
Current assignee: Eaton Corp
Priority date: 2014-03-17
Filing date: 2015-03-17
Publication date: 2019-08-07
Anticipated expiration: 2035-03-17
Also published as: US20170107987A1; CA2943101C; EP3120004A4; CA2943101A1; US10247190B2; WO2015187230A3; WO2015187230A2; EP3120004A2

Description

Background

Current aircraft engine actuation loops use fixed pressure levels of fuel to provide a required force for actuation purposes. These fixed pressure levels are generated using pressure regulators. This is an inefficiency in the system due to the pressure loss from pump discharge down to the regulated supply pressure.
The use of fuel on aircraft engines to drive actuation loops is common. These actuation loops are typically supplied from one or more regulated pressure sources and referenced to the low pressure stage of the fuel pump, commonly a centrifugal stage. The need for a fixed differential pressure, provided by pressure regulators, is driven by control needs to avoid large changes in control gains. In order to generate these fixed pressure differentials, discharge pressure from the pump is regulated or allowed to leak through a valve, or pressure regulator. This leakage is an inefficiency in the fuel system.
WO 2013/025818 A1 and US 2010/0263634 A1 relate to an actuation assembly comprising at least two centrifugal pumps connected in series, a control valve and an associated actuator according to the preamble of claims 1 and 7.

Summary of the Disclosure

The invention relates to an actuation assembly as defined in claim 1 and a method as defined in claim 1 and a method as defined in claim 7. The actuation assembly (and the associated method) includes a multistage centrifugal pump and a first control valve. The control valve receives a first pressure from one of the centrifugal pump stages and communicates the first pressure for optimally operating an associated first actuator.
The actuation assembly further includes a second control valve that receives a second pressure from a different centrifugal pump stage and communicates the second pressure for optimally operating an associated second actuator.
In one arrangement, return passages from each control valve return to the same stage of the multistage centrifugal pump.
In another arrangement, the first control valve receives a first pressure from one of the centrifugal pump stages downstream of a first centrifugal pump stage.
In another arrangement, a return passage from the first control valve communicates with the multistage centrifugal pump upstream of the one centrifugal pump stage, particularly with the multistage centrifugal pump upstream of the one centrifugal pump stage.
The return passage from the first control valve communicates with an inlet of the one centrifugal pump stage, and in another arrangement the first control valve communicates with an inlet of a centrifugal pump stage different than the one centrifugal pump stage.
The actuation assembly can include a positive displacement pump downstream of the multistage centrifugal pump.
In an another embodiment, the actuation assembly further includes a selector valve between the one stage of the multistage centrifugal pump and the first control valve through which pressure is alternately supplied to the first control valve from the one stage and the positive displacement pump.
The selector valve may be pressure activated to initially forward pressure to the first control valve from the positive displacement pump and then switch to forward pressure from the one stage once the outlet pressure from the centrifugal pump has reached a certain level.
A primary benefit is the reduction of inefficiencies in engine actuation loops.
Another advantage relates to the elimination of pressure regulators and the associated leakage of flow therepast associated with conventional systems.
Still another benefit is the ability to establish multiple fixed ratio pressure differentials for various actuator needs.
Yet other advantages are associated with optimizing the pressure level used by the actuators, for example, a reduced number of components, reduced/limited waste flow, and lower cost.
Benefits and advantages of the present disclosure will become more apparent from reading and understanding the following detailed description.

Brief Description of the Drawings

Figure 1 shows a conventional, prior art arrangement.
Figures 2-5 schematically show multi-stage centrifugal pump arrangements for optimizing multiple fixed ratio pressure levels for actuators.

Detailed Description

This disclosure uses a multi-stage centrifugal pump solely, or in conjunction with a positive displacement pump, as an engine main fuel pump. Using a multi-stage centrifugal pump, fixed ratio pressure levels (created between the different pump stages where each stage adds additional energy and pressure to the pumped fluid) are automatically generated and can be used directly by the actuators. This improves the efficiency of the fuel system. Depending on the number of pumping stages, potentially more pressure levels are available for actuation thus allowing for better optimization of the actuators.
The use of multiple centrifugal stages allows for design and optimization of multiple fixed ratio pressure levels. For instance, if there are three centrifugal stages, then there will be three fixed ratio pressures. Typically, the first stage is the reference or drain pressure for the actuators, thereby leaving the remaining stage or stages as supply pressure levels. The ability to have multiple pressure levels allows for additional optimization of the actuation loops without the need for additional pressure regulators. Flow is only drawn from the centrifugal stages when needed therefore improving the efficiency of the system. Additionally, the fixed ratio of pressure allows for conventional control gains.
If the main fuel pump contains only centrifugal stages and there exists a need for actuation movement at low speeds, the pump will need to be motor driven. The use of a positive displacement pump in conjunction with the centrifugal stages allows the system to develop pressure at the low speeds (provided primarily by the positive displacement pump) which can be used to supply the actuation loops. Upon reaching a prescribed level, a shuttle type valve, for example, can be used to transition the system from the positive displacement discharge pressure to the appropriate centrifugal stage discharge pressure.
For example, shown in Figure 1 is an engine main fuel pump 100 that includes a centrifugal stage pump 102 and a positive displacement pump such as gear pump 104. Fuel is inlet from passage or line 106 to the centrifugal stage pump 102, pressurized by the centrifugal stage pump, and outlet via passage 108 where it is introduced into the inlet of the gear pump 104. The gear pump 104 further pressurizes the fluid (fuel) where it is provided to the engine (not shown) via passage 110. In addition, branching from the passage 110 is a passage 120 that leads to one or more pressure regulators (two of which are shown as pressure regulator 122A and pressure regulator 122B) for delivery of fuel at reduced pressure levels for control valves 124A, 124B, respectively, via passages 126A, 126B. It will be understood that the individual pressure regulators 122A, 122B can deliver the pressurized fuel at the same or different pressures to the respective control valves 124A, 124B. Each control valve 124A, 124B communicates via a respective passage 130A, 130B with a respective actuator 128A, 128B. In this manner, fuel at a desired pressure level is delivered to the actuators 128A, 128B.
As noted above, discharge pressure from the pump leaks through the valve or the pressure regulator. This leakage flow is returned from the pressure regulators 122A, 122B through passages 140A, 140B, and from the valves 124A, 124B through passages 142A, 142B to passage 108 where the flow combines with flow from the centrifugal pump 102 that is introduced into the gear pump 104.
The new arrangement of Figure 2 advantageously uses a multi-stage centrifugal pump 202, either alone or with the gear pump 204, in a manner that provides multiple fixed ratio pressure levels. More particularly, the multi-stage centrifugal pump 202 includes a first stage 202A, a second stage 202B, and a third stage 202C arranged in series to incrementally increase the pressure from the first stage to the second stage, and likewise from the second stage to the third stage. Due to the incremental increase in the pressure from one stage to the next, the first stage 202A can be used as the reference pressure, i.e., the return flow from control valves 224A and 224B through passages 242A, 242B, respectively, is directed to the passage 208A disposed between the first and second stages of the multistage centrifugal pump. Inlet pressure to the control valve 224A is taken from passage 208C downstream of the third stage 202C of the centrifugal pump, while inlet pressure to control valve 224B is taken from passage 208B downstream of the second stage 202B of the centrifugal pump. Thus, a greater pressure is provided to the first control valve 224A than to the second control valve 224B in the arrangement of Figure 2. Moreover, the pressure regulators (122A, 122B) required in the embodiment of Figure 1 (because the pressure for the actuators is supplied from downstream of the gear pump 104) are eliminated in the arrangement of Figure 2. Instead, an optimized pressure level from the multistage centrifugal pump is used directly by the actuator, resulting in reduced components or hardware, reduced cost, along with the benefit of reduced or limited waste flow. A further distinction is that with the pressure regulators used in the embodiment of Figure 1, fixed pressure is provided to the control valves which are not as sensitive to the load. On the other hand, the pressure ratios associated with the embodiment of Figure 2 are related to the speed of the pump (i.e., the pressure from the particular centrifugal pump stage is dependent on the rotational speed of the centrifugal pump) and oftentimes the loads on the actuators are also speed dependent.
In the slightly modified embodiment of Figure 3, a two position selector valve or shuttle valve 250 is interposed between the third stage 202C of the centrifugal pump/gear pump 204 and the first control valve 224A. Thus at low speeds, pressure required for the first control valve 224A and the associated actuator 228A is provided from downstream of the gear pump 204, and once the centrifugal pump speed increases (and thus the outlet pressure of the third stage 202C of the centrifugal pump), selector valve 250 moves from the position shown in Figure 3 to a position where pressure from the outlet of the third stage of the centrifugal pump is supplied to the control valve 224A (and to the associated actuator 228A) through the selector valve 250.
Another modification is shown in Figures 4 and 5. Here, the pressure supplied to the control valve 224A comes from the outlet of the third stage 202C of the centrifugal pump. However, the reference pressure for the first control valve 224A is associated with the second stage 202B of the centrifugal pump (and not with the first stage 202A of the centrifugal pump as in the embodiments of Figures 2-3). Thus, one skilled in the art will appreciate that whichever output stage of the multistage centrifugal pump most closely matches the pressure requirements for a particular control valve can be selected, and likewise the pressure differential can be optimized to also meet these requirements. Figure 5 further illustrates the same arrangement of Figure 4 without use of a positive displacement pump, such as the gear pump 204 of Figure 4. In all other respects, the system of Figure 5 is the same.
This written description uses examples to describe the disclosure, including the best mode, and also to enable any person skilled in the art to make and use the disclosure. The patentable scope of the disclosure is defined by the claims, and may include other examples that occur to those skilled in the art.

Claims

An actuation assembly comprising:
a multistage centrifugal pump (202); and

a first control valve (224A) that receives a first pressure from one of the centrifugal pump stages (202C) and communicates the first pressure for optimally operating an associated first actuator (228A), characterized by a second control valve (224B) that receives a second pressure from a different centrifugal pump stage (202B) and communicates the second pressure for optimally operating an associated second actuator (228B).
The actuation assembly of claim 1 wherein return passages (242A, 242B) from each control valve (224A, 224B) return to the same stage (202B) of the multistage centrifugal pump (202).
The actuation assembly of claim 1 wherein the first control valve (224A) receives the first pressure from one of the centrifugal pump stages (202C) downstream of a first centrifugal pump stage (202A).
The actuation assembly of claim 1 wherein a return passage (242A) from the first control valve (224A) communicates with the multistage centrifugal pump (20) upstream of the one centrifugal pump stage (202C).
The actuation assembly of claim 4 wherein the return passage (242A, 242A') from the first control valve (224A) communicates with an inlet of one of (i) the one centrifugal pump stage (202C), or (ii) a centrifugal pump stage (202B) different than the one centrifugal pump stage.
The actuation assembly of claim 1 further comprising a positive displacement pump (204) downstream of the multistage centrifugal pump (202);
the assembly comprising a selector valve (250) between the one stage (202C) of the multistage centrifugal pump (202) and the first control valve (224A) through which pressure is alternately supplied to the first control valve from the one stage and the positive displacement pump,
wherein further the selector valve is pressure activated to initially forward pressure to the first control valve (224A) from the positive displacement pump and then switch to forward pressure from the one stage once the outlet pressure from the centrifugal pump has reached a certain level.
A method of operating an actuator comprising:
providing a multistage centrifugal pump (202); and

directing a first pressure from one stage (202C) of the multistage centrifugal pump to a first control valve (224A) for optimally operating an associated first actuator (228A) associated with the first control valve,

characterized by providing a second control valve (224B) that receives a second pressure from a different centrifugal pump stage (202B) ; and communicating the second pressure for optimally operating an associated second actuator (228B).
The method of claim 7 further comprising providing return passages (242A, 242B) from each control valve (224A, 224B) to the same stage (202B) of the multistage centrifugal pump (202).
The method of claim 7 further comprising directing the first pressure from one of the centrifugal pump stages (202C) downstream of a first centrifugal pump stage (202A) to the first control valve.
The method of claim 7 further comprising providing a return passage (242A, 242A') from the first control valve (224A) that communicates with the multistage centrifugal pump (202) upstream of the one centrifugal pump stage (202C), and connecting the return passage from the first control valve with an inlet of either (i) the one centrifugal pump stage or (ii) a centrifugal pump stage (202B) different than the one centrifugal pump stage.
The method of claim 7 further comprising providing a positive displacement pump (204) downstream of the multistage centrifugal pump (202).
The method of claim 11 further comprising providing a selector valve (250) between the one stage (202C) of the multistage centrifugal pump (202) and the first control valve (224A) through which pressure is alternately supplied to the first control valve from the one stage and the positive displacement pump (204).
The method of claim 12 wherein the selector valve (250) is pressure activated and initially forwarding pressure to the first control valve (224A) from the positive displacement pump (204) and then switching to forward pressure from the one stage (202C) once the outlet pressure from the centrifugal pump (202) has reached a certain level.